US4095965A - Absorption filter - Google Patents
Absorption filter Download PDFInfo
- Publication number
- US4095965A US4095965A US05/711,536 US71153676A US4095965A US 4095965 A US4095965 A US 4095965A US 71153676 A US71153676 A US 71153676A US 4095965 A US4095965 A US 4095965A
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- United States
- Prior art keywords
- filter
- section
- substrate
- absorption
- bypass
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- Expired - Lifetime
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- 238000010521 absorption reaction Methods 0.000 title claims abstract description 40
- 239000000356 contaminant Substances 0.000 claims abstract description 21
- 231100000331 toxic Toxicity 0.000 claims abstract description 5
- 230000002588 toxic effect Effects 0.000 claims abstract description 5
- 230000002285 radioactive effect Effects 0.000 claims abstract description 4
- 238000000746 purification Methods 0.000 claims abstract description 3
- 239000000758 substrate Substances 0.000 claims description 20
- 239000000523 sample Substances 0.000 claims description 9
- 238000012544 monitoring process Methods 0.000 claims description 6
- 238000005452 bending Methods 0.000 claims description 3
- 238000001914 filtration Methods 0.000 description 9
- 238000011109 contamination Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 230000001960 triggered effect Effects 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
- B01D53/0415—Beds in cartridges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0454—Controlling adsorption
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/02—Treating gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/93—Toxic compounds not provided for in groups B01D2257/00 - B01D2257/708
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40084—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by exchanging used adsorbents with fresh adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/404—Further details for adsorption processes and devices using four beds
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S55/00—Gas separation
- Y10S55/09—Radioactive filters
Definitions
- the invention is concerned with an absorption filter for the purification of gas or air streams, especially such gas or air streams containing toxic or radioactive contaminants.
- Absorption filters of this type are familiar in many different design versions. They consist of at least one filter chamber, which is characterized by featuring gas-permeable walls, arranged traverse to the direction of flow.
- the filter chambers conventionally consist of a prismatic housing, capable of being charged from the top with a granular absorption medium.
- the absorption medium in turn, can be removed from the bottom of the housing after having reached a certain degree of saturation, while fresh substrate is being added from the top.
- the filter chamber housing is equipped on one side with an adapter for the contaminated air and on the other side with an exit pipe for the purified air.
- the feed pipe and exit pipe are joined to each other by a bypass line which is parallel to the absorption medium of the filter chamber and is also filled with the absorption substrate.
- This bypass filter section allows for monitoring the degree of saturation of the absorption substrate contained in the filter chamber by removing the filter medium from the bypass filter section.
- the contaminants carried by the gas or air stream, passing through the absorption filter, are progressively removed from the supply side of the chamber to the exit side. Since the contaminated gas or air streams always contain several different types of gaseous contaminants (which are absorbed by the filter medium with markedly different degrees of effectiveness), it is of extreme importance, especially in the presence of toxic or radioactive contaminants in gaseous form, to absorb these materials first in the filter medium, both with respect to time and location. It is also important to remove the more difficultly absorbed gaseous contaminants at regions which are closer to the exit side of the purified gas stream. It is especially important that the effectiveness of removal of these contaminants is not impaired in this region by the presence of the more easily absorbed contaminants. In other words, care must be taken to preserve a region of sufficient capacity near the pure air exit side for the absorption of gaseous contaminants in which none of the more easily absorbed contaminants are present.
- an absorption filter has been designed (West German Patent No. DT-OS No. 2,239,827), which features an additional gas-permeable divider in the approximate center of the filter chamber, thus providing for two sequential chambers in series within one housing.
- the filter medium in both chambers is in direct contact with the central gas-permeable divider section. Both chamber sections can be individually and separately charged with the filter medium.
- the advantage of this design feature is to be found in the fact that the filter medium from the first section, initially exposed to the contaminated gas stream, can be seperately removed and replaced by fresh substrate without also having to empty the second chamber where the filter medium has not yet reached a degree of saturation requiring recharge.
- the bypass filters serve as control filters and are arranged parallel to the filter housing and are also filled with filter medium.
- the bypass filter is exposed to the same gas stream; their filtration thickness is identical to the filter medium contained in the main chamber.
- This objective is achieved, according to the instant invention, by a design which provides for partial chambers according to the state of the art, featuring gas-permeable walls and, in addition, provides for a U-shaped frame interposed between the frame housing and between the chambers. Located in this U-shaped spacer frame section are sensing or measurement probes capable of continuously indicating the degree of saturation of the partial chamber closest to the entry side of the contaminated air stream. These measurement probes are in themselves known and are capable of monitoring the free space between chamber sections without any time delay, so that a break through of contaminants of the more easily absorbed type can be immediately registered; and any contamination of the downstream filter section, which would impair the capacity of this section to absorb the more difficultly removable contaminants, can thus be instantly prevented. A timely exchange of the filter medium in the upstream chamber section can thus be carried out without interrupting the filtration process.
- a bypass filter section which is filled with the filtration medium and which is parallel to the feed line, or respectively the exit line, and has an absorption length which corresponds to the absorption capacity of the respective chamber section.
- the absorption distance of the bypass filter section consists of a series of cartridges, arranged sequentially in chambers, which are filled with the absorption medium.
- bypass filtration section features two parallel filtration lines, which can be isolated from each other.
- This parallel arrangement of two bypass sections allows for monitoring without interruption, since during removal of one bypass section, by respective manipulation of the valves, the other section can be put in service.
- FIG. 1 is a front view of an absorption filter constructed according to the principles of the present invention
- FIG. 2 is a right side elevational view of FIG. 1 demonstrating two absorption filters in parallel arrangement
- FIG. 3 is a modified design of the filter illustrated in FIG. 2;
- FIG. 4 is an expanded sectional presentation of FIG. 3.
- FIGS. 1 and 2 wherein there is illustrated one example of the present invention in the form of two parallel absorption filters A and B, each of which has two housings 1 and 2 which are closed off on both sides by the gas-permeable, perforated sheets 21, or respectively 22 (FIG. 4).
- Each housing is equipped with a topside feeding adaptor for a granular absorption substrate 19, such as an active charcoal (FIG. 3), and a bottom side discharge adapter 4 used to remove the exhausted absorption substrate 19 from the housings 1 and 2, while simultaneously recharging fresh absorption substrate 19 through adapter 3.
- a topside feeding adaptor for a granular absorption substrate 19, such as an active charcoal (FIG. 3) and a bottom side discharge adapter 4 used to remove the exhausted absorption substrate 19 from the housings 1 and 2, while simultaneously recharging fresh absorption substrate 19 through adapter 3.
- a circumferential, U-shaped frame 8 is provided, joining the two housings 1 and 2 to each other in air-tight fashion and providing for an empty intermediate section.
- the contaminated air stream is charged to, respectively, absorption filter A or B, via feed line 5, which is arranged on the outside of housing 1.
- the clean air is removed via off-gas line 6, itself attached to the outside of housing 2.
- Absorption filter A, or respectively B is mounted on frame 7.
- the air stream to be cleaned enters housing 1, via feed line 5, passes into housing 2 through the intermediate space provided by the U-shaped frame 8, and exits as a pure air steam from off-gas line 6.
- the intermediate space, provided by frame 8, contains a sensing probe 9, which monitors the degree of saturation of the air stream exiting from housing 1.
- the same probe 9 indicates the degree of saturation of this air stream in continuous fashion on a respective instrument 16, so that the filtration substrate 19, on reaching a predetermined degree of saturation, can be discharged from housing 1 and be replaced by fresh absorption material.
- the monitoring instrument 16 activates an optical or acoustical warning signal or may interrupt the further contaminated air supply, such positive interference to be triggered by reaching a preset degree of saturation of the air stream monitored by the probe.
- a bypass filter line 10 is arranged, which serves as a control section for housing 1; similarly, between U-shaped frame 8 and the exit line 6, a second bypass line 11 is provided, serving as control for housing 2.
- Each bypass line 10 and 11 provides for two separate filled absorption lines 12 and 13, which correspond in lengths to the capacity of the filtration substrate layers in housings 1 and 2 and can be separately closed off by valves 14 so that either one of the sections 12 or 13 can be used to determine the degree of saturation.
- the filled sections 12 and 13 are subdivided into separate, sequentially arranged chambers 12a and 13a, containing the cartridges filled with filtration substrate 19, which can be removed from chambers 12a and 13a to determine the degree of saturation.
- FIG. 4 shows, inside the U-shaped frame 8 a second U-shaped frame 20 is installed on the two legs of which the perforated screens 21 and 22 are fastened.
- the U-shaped frame 8 contains the structural support elements 23, which prevent a bending of perforated screens 21 and 22 towards the inside and, thus, provide for trouble-free functioning of both the monitoring and recording probe, as well as proper functioning of the bypass sections 10 and 11.
- the perforated screens 21 and 22 form the inner gas-permeable walls of housings 1 and 2, due to the fact that U-shaped frame 8 is joined in air-tight fashion with housings 1 and 2 by a bolt 25 passing through flange 24 of frame 8 and housings 1 and 2.
- FIG. 4 does not show the sensing or recording probe 9.
- FIG. 3 demonstrates a modified design version of absorption filter A, due to the fact that in place of feed line 5 and off-gas line 6, in line with FIG. 2, the coaxial feed lines 17 and off-gas lines 18 are provided.
- the external perforated screens 21 and 22 of housings 1 and 2 in this case are fastened to the feed line adapter 17 and off-gas line adapter 18 and in assembly form the gas-permeable external walls of housings 1 and 2.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Separation Of Gases By Adsorption (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
An absorption filter for the purification of gas or air streams, especially gas or air streams which contain toxic or radioactive contaminants.
Description
I. Field of the Invention
The invention is concerned with an absorption filter for the purification of gas or air streams, especially such gas or air streams containing toxic or radioactive contaminants.
II. Description of the Prior Art
Absorption filters of this type are familiar in many different design versions. They consist of at least one filter chamber, which is characterized by featuring gas-permeable walls, arranged traverse to the direction of flow. The filter chambers conventionally consist of a prismatic housing, capable of being charged from the top with a granular absorption medium. The absorption medium, in turn, can be removed from the bottom of the housing after having reached a certain degree of saturation, while fresh substrate is being added from the top. Thus, the filter chamber can remain in virtually uninterrupted service. The filter chamber housing is equipped on one side with an adapter for the contaminated air and on the other side with an exit pipe for the purified air. The feed pipe and exit pipe are joined to each other by a bypass line which is parallel to the absorption medium of the filter chamber and is also filled with the absorption substrate. This bypass filter section allows for monitoring the degree of saturation of the absorption substrate contained in the filter chamber by removing the filter medium from the bypass filter section.
The contaminants carried by the gas or air stream, passing through the absorption filter, are progressively removed from the supply side of the chamber to the exit side. Since the contaminated gas or air streams always contain several different types of gaseous contaminants (which are absorbed by the filter medium with markedly different degrees of effectiveness), it is of extreme importance, especially in the presence of toxic or radioactive contaminants in gaseous form, to absorb these materials first in the filter medium, both with respect to time and location. It is also important to remove the more difficultly absorbed gaseous contaminants at regions which are closer to the exit side of the purified gas stream. It is especially important that the effectiveness of removal of these contaminants is not impaired in this region by the presence of the more easily absorbed contaminants. In other words, care must be taken to preserve a region of sufficient capacity near the pure air exit side for the absorption of gaseous contaminants in which none of the more easily absorbed contaminants are present.
In order to provide for a solution to this problem, an absorption filter has been designed (West German Patent No. DT-OS No. 2,239,827), which features an additional gas-permeable divider in the approximate center of the filter chamber, thus providing for two sequential chambers in series within one housing. The filter medium in both chambers is in direct contact with the central gas-permeable divider section. Both chamber sections can be individually and separately charged with the filter medium. The advantage of this design feature is to be found in the fact that the filter medium from the first section, initially exposed to the contaminated gas stream, can be seperately removed and replaced by fresh substrate without also having to empty the second chamber where the filter medium has not yet reached a degree of saturation requiring recharge. The exact determination of the time when replacement of the filter medium in the first chamber section is required can, however, not be made in the case of this state of the art design version, thus allowing for the danger that the chamber section intended for the absorption of the more difficultly removed contaminants will be contaninated from the direction of the saturated previous chamber section with the more easily absorbed contaminants and, thus, no longer allowing for an unambiguous guarantee that the more difficultly absorbed gaseous contaminants can be absorbed in the chamber section situated close to the pure air exit line. For the determination of the degree of saturation for this design version, only the familiar bypass filter section is available, which runs parallel to the adjoining chamber sections and bridges them and, therefore, is unable to provide any information concerning the degree of saturation of the chamber section close to the feed air side of the total assembly. The bypass filters serve as control filters and are arranged parallel to the filter housing and are also filled with filter medium. The bypass filter is exposed to the same gas stream; their filtration thickness is identical to the filter medium contained in the main chamber. By removing the bypass filter section, followed by analysis of the absorption medium, conclusions can be drawn with respect to the saturation state of the filter medium in the main chamber. This method is awkward, and information concerning the saturation of the filter medium with the more easily absorbed contaminants can only be obtained, if at all, with the time delay inherent in dismantling the bypass section and carrying out the analysis required. During this period the more easily absorbed contaminants could saturate the chamber section close to the contaminated air entry side, break through into the adjoining chamber section, and contaminate this half of the total assembly by enrichment with the easily absorbed components and, thus, impairing the trouble-free absorption of the more difficultly absorbed, toxic, gaseous contaminants.
It is the object of the instant invention to overcome this disadvantage, which is inherent to the state of the art design of filters consisting of subdivided partial chambers. It is furthermore the object of the invention to improve an absorption filter, featuring subdivided partial chambers, in such a manner as to allow for reliable and timely information available without undue loss of time, concerning the degree of saturation of the chamber section closest to the entry side of the contaminated air stream. Thus, an exchange of the filtration medium in this partial section of the filter guarantees an assured removal of the more difficultly removed contaminants in the respective filter section and positively prevents its contamination by the more easily absorbed contaminants.
This objective is achieved, according to the instant invention, by a design which provides for partial chambers according to the state of the art, featuring gas-permeable walls and, in addition, provides for a U-shaped frame interposed between the frame housing and between the chambers. Located in this U-shaped spacer frame section are sensing or measurement probes capable of continuously indicating the degree of saturation of the partial chamber closest to the entry side of the contaminated air stream. These measurement probes are in themselves known and are capable of monitoring the free space between chamber sections without any time delay, so that a break through of contaminants of the more easily absorbed type can be immediately registered; and any contamination of the downstream filter section, which would impair the capacity of this section to absorb the more difficultly removable contaminants, can thus be instantly prevented. A timely exchange of the filter medium in the upstream chamber section can thus be carried out without interrupting the filtration process.
It is a further characteristic of the instant invention to provide for the possibility of an optical or acoustical warning signal and/or an interruption of the contaminated air feed, based on reaching a degree of saturation corresponding to exhaustion of the absorption capacity in the upstream chamber section.
It is furthermore essential for the present invention that on both sides of the U-shaped frame perforated, gas-pervious sheeting is provided which is structurally secured against bending by support brackets. In line with the features, according to the instant invention, the arrangement of the gas-permeable walls between the two chamber sections on the U-frame allows for trouble-free and easy mounting, as well as easy cleaning of the filter chambers.
It is a further characteristic of the instant invention to provide for a bypass filter section, which is filled with the filtration medium and which is parallel to the feed line, or respectively the exit line, and has an absorption length which corresponds to the absorption capacity of the respective chamber section. Based on the feature of the U-shaped frame, spaced between the filter chambers, it is readily possible to provide for a bypass section for each individual chamber section. To this effect the entry feed pipe connects to the inside of the U-shaped frame on the one hand, while for the other bypass section, the inside of the U-shaped frame is connected with the exit pipe section. By these means a simple separate control of the filter media in each partial chamber is readily possible.
It is furthermore significant that the absorption distance of the bypass filter section consists of a series of cartridges, arranged sequentially in chambers, which are filled with the absorption medium.
It is furthermore essential to the instant invention that the bypass filtration section features two parallel filtration lines, which can be isolated from each other. This parallel arrangement of two bypass sections allows for monitoring without interruption, since during removal of one bypass section, by respective manipulation of the valves, the other section can be put in service.
Other objects, advantages and applications of the present invention will be seen by those skilled in the art of filters when the accompanying description of several examples of the best modes contemplated for practicing the invention is read in conjunction with the description of the accompanying drawings.
The attached drawings show an exemplary design according to the invention wherein like reference numerals refer to like components throughout the several figures, and wherein:
FIG. 1 is a front view of an absorption filter constructed according to the principles of the present invention;
FIG. 2 is a right side elevational view of FIG. 1 demonstrating two absorption filters in parallel arrangement;
FIG. 3 is a modified design of the filter illustrated in FIG. 2; and
FIG. 4 is an expanded sectional presentation of FIG. 3.
Referring now to the drawings and, in particular, to FIGS. 1 and 2 wherein there is illustrated one example of the present invention in the form of two parallel absorption filters A and B, each of which has two housings 1 and 2 which are closed off on both sides by the gas-permeable, perforated sheets 21, or respectively 22 (FIG. 4). Each housing is equipped with a topside feeding adaptor for a granular absorption substrate 19, such as an active charcoal (FIG. 3), and a bottom side discharge adapter 4 used to remove the exhausted absorption substrate 19 from the housings 1 and 2, while simultaneously recharging fresh absorption substrate 19 through adapter 3. Between the two housings 1 and 2, a circumferential, U-shaped frame 8 is provided, joining the two housings 1 and 2 to each other in air-tight fashion and providing for an empty intermediate section. The contaminated air stream is charged to, respectively, absorption filter A or B, via feed line 5, which is arranged on the outside of housing 1. In turn, the clean air is removed via off-gas line 6, itself attached to the outside of housing 2. Absorption filter A, or respectively B, is mounted on frame 7. The air stream to be cleaned enters housing 1, via feed line 5, passes into housing 2 through the intermediate space provided by the U-shaped frame 8, and exits as a pure air steam from off-gas line 6. The intermediate space, provided by frame 8, contains a sensing probe 9, which monitors the degree of saturation of the air stream exiting from housing 1. The same probe 9 indicates the degree of saturation of this air stream in continuous fashion on a respective instrument 16, so that the filtration substrate 19, on reaching a predetermined degree of saturation, can be discharged from housing 1 and be replaced by fresh absorption material. In order to guarantee the reliable exchange of filter medium in housing 1, the monitoring instrument 16 activates an optical or acoustical warning signal or may interrupt the further contaminated air supply, such positive interference to be triggered by reaching a preset degree of saturation of the air stream monitored by the probe. Between feed line 5 and the U-shaped frame 8, a bypass filter line 10 is arranged, which serves as a control section for housing 1; similarly, between U-shaped frame 8 and the exit line 6, a second bypass line 11 is provided, serving as control for housing 2. This allows for separate control of housings 1 and 2 by means of the bypass sections 10 and 11. Each bypass line 10 and 11 provides for two separate filled absorption lines 12 and 13, which correspond in lengths to the capacity of the filtration substrate layers in housings 1 and 2 and can be separately closed off by valves 14 so that either one of the sections 12 or 13 can be used to determine the degree of saturation. The filled sections 12 and 13 are subdivided into separate, sequentially arranged chambers 12a and 13a, containing the cartridges filled with filtration substrate 19, which can be removed from chambers 12a and 13a to determine the degree of saturation.
As FIG. 4 shows, inside the U-shaped frame 8 a second U-shaped frame 20 is installed on the two legs of which the perforated screens 21 and 22 are fastened. The U-shaped frame 8 contains the structural support elements 23, which prevent a bending of perforated screens 21 and 22 towards the inside and, thus, provide for trouble-free functioning of both the monitoring and recording probe, as well as proper functioning of the bypass sections 10 and 11. During assembly of absorption filter A, or respectively B, the perforated screens 21 and 22 form the inner gas-permeable walls of housings 1 and 2, due to the fact that U-shaped frame 8 is joined in air-tight fashion with housings 1 and 2 by a bolt 25 passing through flange 24 of frame 8 and housings 1 and 2. FIG. 4 does not show the sensing or recording probe 9.
FIG. 3 demonstrates a modified design version of absorption filter A, due to the fact that in place of feed line 5 and off-gas line 6, in line with FIG. 2, the coaxial feed lines 17 and off-gas lines 18 are provided. The external perforated screens 21 and 22 of housings 1 and 2 in this case are fastened to the feed line adapter 17 and off-gas line adapter 18 and in assembly form the gas-permeable external walls of housings 1 and 2.
While two embodiments of the present invention have been disclosed, it should be understood by those skilled in the art that other forms of the invention may be had, all coming within the spirit of the invention and scope of the appended claims.
Claims (6)
1. An absorption filter for the purification of gas and/or airstreams, especially those containing toxic or radioactive contaminants, said absorption filter comprising:
a filter housing having an inlet and an outlet and first and second filter chambers, each charged with a granular absorption substrate, said housing inlet communicating with said first filter chamber and said outlet communicating with said second filter chamber, each filter chamber having transverse gas-permeable walls, said first and second filter chambers being separately chargeable with said substrate, said filter chambers being disposed in series in the direction of gas flow, an intermediate section joining said first and second filter chambers in an air-tight fashion such that the flow is from said inlet through said first filter chamber to said second filter chamber via said intermediate section and exhausted through said outlet;
a sensing probe disposed in said intermediate section to monitor the degree of saturation of the substrate in said first filter chamber;
a monitoring instrument connected to said probe and responsive to a predetermined degree of saturation of said substrate in said first filter chamber for triggering a warning signal; and
a bypass filter section having an inlet connected to said housing inlet and an outlet connected to said intermediate section and filled with an absorption substrate, the length of said bypass filter section corresponding to the absorptive capacity of the filter substrate in said first filter chamber.
2. The filter defined in claim 1 wherein said intermediate section comprises a U-shaped frame which joins said first and second filter chambers in said air-tight fashion, said U-shaped frame having perforated sheeting on both sides thereof, said perforated sheeting forming the walls of said first and second filter chambers; and
internal, structural support members supporting said walls against bending.
3. The filter defined in claim 1 wherein said bypass filter section comprises a series of cartridges arranged sequentially in subchambers which are filled with said absorption substrate.
4. The filter defined in claim 1 further comprising a second bypass filter section having an inlet connected to said intermediate section and an outlet connected to the outlet of said second filter chamber, said second bypass filter section being filled with an absorption substrate, the length of said second bypass filter section corresponding to the absorptive capacity of the filter substrate in said second filter chamber.
5. The filter defined in claim 4 wherein said second bypass filter section comprises a series of cartridges, arranged sequentially in subchambers which are filled with said absorption substrate.
6. The filter defined in claim 1 wherein said bypass filter section comprises two parallel, separately usable subsections; and
valve means communicating with said separable subsections for selectively and individually opening and closing said subsections.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DT7527377 | 1975-08-27 | ||
DE7527377U DE7527377U (en) | 1975-08-27 | 1975-08-27 | ADSORPTION FILTER FOR CLEANING IN PARTICULAR TOXIC OR RADIOACTIVE POLLUTIONS CONTAINING GAS OR AIR FLOWS |
Publications (1)
Publication Number | Publication Date |
---|---|
US4095965A true US4095965A (en) | 1978-06-20 |
Family
ID=6655071
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US05/711,536 Expired - Lifetime US4095965A (en) | 1975-08-27 | 1976-08-04 | Absorption filter |
Country Status (3)
Country | Link |
---|---|
US (1) | US4095965A (en) |
DE (1) | DE7527377U (en) |
FR (1) | FR2322510A7 (en) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4626265A (en) * | 1985-06-17 | 1986-12-02 | Pall Corporation | Purification system |
US4847594A (en) * | 1988-03-28 | 1989-07-11 | Transducer Research, Inc. | Sensor for detecting the exhaustion of an adsorbent bed |
US5169419A (en) * | 1991-01-18 | 1992-12-08 | Ebara Corporation | Gas adsorber for exhaust gas |
US5334237A (en) * | 1993-02-26 | 1994-08-02 | Saes Pure Gas, Inc. | Method and apparatus for predicting end-of-life of a consumable in a fluid purification system |
DE4447196A1 (en) * | 1994-12-30 | 1996-07-11 | Kurt M Dr Ing Pohl | Appts. for redn. of pollutants in fluid flows |
US5685895A (en) * | 1994-08-10 | 1997-11-11 | Nikon Corporation | Air cleaning apparatus used for an exposure apparatus |
US5716427A (en) * | 1995-08-21 | 1998-02-10 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Equipment for gas separation by adsorption |
US5759242A (en) * | 1996-07-23 | 1998-06-02 | Praxair Technology, Inc. | Radial bed vaccum/pressure swing adsorber vessel |
US5824139A (en) * | 1994-11-14 | 1998-10-20 | Steag Aktiengesellschaft | Adsorber for purifying combustion gases |
US6142742A (en) * | 1994-10-31 | 2000-11-07 | Saes Pure Gas, Inc. | Getter pump module and system |
US6168645B1 (en) * | 1997-10-15 | 2001-01-02 | Saes Getters S.P.A. | Safety system for gas purifier |
US6797042B2 (en) | 2002-06-21 | 2004-09-28 | Pyramid Air Solutions, Inc. | Pyramid air cleaner |
US20060207426A1 (en) * | 2005-03-17 | 2006-09-21 | Industrial Pipeline Solutions Usa L.L.C. | Filter assembly for pipelines |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2515976B2 (en) * | 1981-06-18 | 1988-05-13 | Poelman Sofiltra | COMPACT INSTALLATION FOR CONTAMINATED FLUID FILTRATION |
FR2507913B1 (en) * | 1981-06-18 | 1987-03-27 | Poelman Sofiltra | COMPACT INSTALLATION FOR CONTAMINATED FLUID FILTRATION |
DE9312523U1 (en) * | 1993-05-03 | 1993-11-04 | KesslerTech GmbH, 35394 Gießen | Device for monitoring the service life of filter devices in ventilation and air conditioning systems |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US561203A (en) * | 1896-06-02 | Frederick southwell cripps | ||
US2033665A (en) * | 1934-03-26 | 1936-03-10 | William H Rees | Means for controlling dewpoint |
GB480507A (en) * | 1936-07-11 | 1938-02-23 | Pirelli | Improvements relating to filters and purifiers employed for conditioning air, for example for respiration, or other gas by freeing it from poisonous gases and other injurious or undesired constitutents |
US3330101A (en) * | 1966-03-30 | 1967-07-11 | American Air Filter Co | Particulate-type fluid-treating filter assembly |
US3765225A (en) * | 1972-10-30 | 1973-10-16 | American Air Filter Co | Carbon filter leak detector |
US3778799A (en) * | 1972-03-28 | 1973-12-11 | Cables De Lyon Geoffroy Delore | Safety device for pipe lines under gas pressure |
US3868237A (en) * | 1972-05-05 | 1975-02-25 | Wolfgang Berz | Dust filter |
-
1975
- 1975-08-27 DE DE7527377U patent/DE7527377U/en not_active Expired
-
1976
- 1976-07-23 FR FR7623122A patent/FR2322510A7/en not_active Expired
- 1976-08-04 US US05/711,536 patent/US4095965A/en not_active Expired - Lifetime
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US561203A (en) * | 1896-06-02 | Frederick southwell cripps | ||
US2033665A (en) * | 1934-03-26 | 1936-03-10 | William H Rees | Means for controlling dewpoint |
GB480507A (en) * | 1936-07-11 | 1938-02-23 | Pirelli | Improvements relating to filters and purifiers employed for conditioning air, for example for respiration, or other gas by freeing it from poisonous gases and other injurious or undesired constitutents |
US3330101A (en) * | 1966-03-30 | 1967-07-11 | American Air Filter Co | Particulate-type fluid-treating filter assembly |
US3778799A (en) * | 1972-03-28 | 1973-12-11 | Cables De Lyon Geoffroy Delore | Safety device for pipe lines under gas pressure |
US3868237A (en) * | 1972-05-05 | 1975-02-25 | Wolfgang Berz | Dust filter |
US3765225A (en) * | 1972-10-30 | 1973-10-16 | American Air Filter Co | Carbon filter leak detector |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4626265A (en) * | 1985-06-17 | 1986-12-02 | Pall Corporation | Purification system |
US4847594A (en) * | 1988-03-28 | 1989-07-11 | Transducer Research, Inc. | Sensor for detecting the exhaustion of an adsorbent bed |
US5169419A (en) * | 1991-01-18 | 1992-12-08 | Ebara Corporation | Gas adsorber for exhaust gas |
US5334237A (en) * | 1993-02-26 | 1994-08-02 | Saes Pure Gas, Inc. | Method and apparatus for predicting end-of-life of a consumable in a fluid purification system |
US5685895A (en) * | 1994-08-10 | 1997-11-11 | Nikon Corporation | Air cleaning apparatus used for an exposure apparatus |
US6142742A (en) * | 1994-10-31 | 2000-11-07 | Saes Pure Gas, Inc. | Getter pump module and system |
US5824139A (en) * | 1994-11-14 | 1998-10-20 | Steag Aktiengesellschaft | Adsorber for purifying combustion gases |
DE4447196C2 (en) * | 1994-12-30 | 1998-01-22 | Kurt M Dr Ing Pohl | Device for monitoring adsorption filter systems |
DE4447196A1 (en) * | 1994-12-30 | 1996-07-11 | Kurt M Dr Ing Pohl | Appts. for redn. of pollutants in fluid flows |
US5716427A (en) * | 1995-08-21 | 1998-02-10 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Equipment for gas separation by adsorption |
US5759242A (en) * | 1996-07-23 | 1998-06-02 | Praxair Technology, Inc. | Radial bed vaccum/pressure swing adsorber vessel |
US6168645B1 (en) * | 1997-10-15 | 2001-01-02 | Saes Getters S.P.A. | Safety system for gas purifier |
US6797042B2 (en) | 2002-06-21 | 2004-09-28 | Pyramid Air Solutions, Inc. | Pyramid air cleaner |
US20060207426A1 (en) * | 2005-03-17 | 2006-09-21 | Industrial Pipeline Solutions Usa L.L.C. | Filter assembly for pipelines |
US7223298B2 (en) | 2005-03-17 | 2007-05-29 | Pgr Filters, L.L.C. | Filter assembly for pipelines |
Also Published As
Publication number | Publication date |
---|---|
DE7527377U (en) | 1976-06-10 |
FR2322510A7 (en) | 1977-03-25 |
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